Biotreatment of Industrial Effluents

Nomenclature

a

gas-liquid interfacial area (gas area per unit liquid volume)

BOD

biological oxygen demand

C L

liquid phase concentration

liquid phase concentration that is in equilibrium with the gas phase

C x

concentration of pollutant at distance x

d

bubble diameter

d P

particle diameter

D i

impeller diameter

D T

tank diameter

E

activation energy

f

recycle ratio

J D

Coulburn j factor

M A

molecular weight of solute

M B

molecular weight of solvent

N H

Ammonical nitrogen removed (kg/day)

N Pe

Peclet number

N Re

Reynolds number

N Sc

Schmidt number

N T

Total nitrogen removed (kg/day)

q o

feed flow rate

Q

toxic release rate, g/s

R

endogeneous respiration rate (3.9 mg O 2/g MLSS /h)

R

Gas constant

S

substrate concentration in the exit stream

S o

substrate concentration in the exit stream

T

temperature

U

wind speed, m/s

U mf

minimum fluidization velocity

V

reactor or aeration tank volume (m 3)

V A

molar volume of solute

X

cell concentration

Y

yield coefficient

?

bed porosity

? g

bubble volume to reactor liquid volume

?

Monod specific growth rate

? B

viscosity of solvent

? max K s

Monod constants

?

Association factor (1-2.6)

?

residence time

? c

sludge age

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Category: Industrial Gases
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